Polymerization process for forming polymeric ultrathin conformal coatings on electrode materials

ABSTRACT

An electroactive material for use in an electrochemical cell, like a lithium ion battery, is provided. The electroactive material comprises silicon or tin and undergoes substantial expansion during operation of a lithium ion battery. A polymeric ultrathin conformal coating is formed over a surface of the electroactive material. The coating is flexible and is capable of reversibly elongating by at least 250% from a contracted state to an expanded state in at least one direction to minimize or prevent fracturing of the negative electrode material during lithium ion cycling. The coating may be applied by vapor precursors reacting in atomic layer deposition (ALD) to form conformal ultrathin layers over the electroactive materials. Methods for making such materials and using such materials in electrochemical cells are likewise provided.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. patent application Ser. No.15/160,377 filed on May 20, 2016, which issued as U.S. Pat. No.10,396,360. The entire disclosure of the above application isincorporated herein by reference.

FIELD

The present disclosure relates to electrode materials forelectrochemical devices, and more particularly to high performancesilicon-containing or tin-containing electrodes having polymericultrathin conformal coatings for lithium ion electrochemical devices andmethods for making such electrodes having polymeric ultrathin conformalcoatings, including by layer-by-layer polymerization process with vaporprecursors.

BACKGROUND

This section provides background information related to the presentdisclosure which is not necessarily prior art.

High-energy density, electrochemical cells, such as lithium ionbatteries and lithium sulfur batteries can be used in a variety ofconsumer products and vehicles, such as Hybrid Electric Vehicles (HEVs)and Electric Vehicles (EVs). Typical lithium ion and lithium sulfurbatteries comprise a first electrode (e.g., a cathode), a secondelectrode (e.g., an anode), an electrolyte material, and a separator.Often a stack of battery cells are electrically connected to increaseoverall output. Conventional lithium ion and lithium sulfur batteriesoperate by reversibly passing lithium ions between the negativeelectrode and the positive electrode. A separator and an electrolyte aredisposed between the negative and positive electrodes. The electrolyteis suitable for conducting lithium ions and may be in solid or liquidform. Lithium ions move from a cathode (positive electrode) to an anode(negative electrode) during charging of the battery, and in the oppositedirection when discharging the battery.

Contact of the anode and cathode materials with the electrolyte cancreate an electrical potential between the electrodes. When electroncurrent is generated in an external circuit between the electrodes, thepotential is sustained by electrochemical reactions within the cells ofthe battery. Each of the negative and positive electrodes within a stackis connected to a current collector (typically a metal, such as copperfor the anode and aluminum for the cathode). During battery usage, thecurrent collectors associated with the two electrodes are connected byan external circuit that allows current generated by electrons to passbetween the electrodes to compensate for transport of lithium ions.

Typical electrochemically active materials for forming an anode includelithium-graphite intercalation compounds, lithium-silicon alloyingcompounds, lithium-tin alloying compounds, lithium alloys. Whilegraphite compounds are most common, recently, anode materials with highspecific capacity (in comparison with conventional graphite) are ofgrowing interest. For example, silicon has the highest known theoreticalcharge capacity for lithium, making it one of the most promisingmaterials for rechargeable lithium ion batteries. However, current anodematerials comprising silicon suffer from significant drawbacks. Thelarge volume changes (e.g., volume expansion/contraction) ofsilicon-containing materials during lithium cycling (e.g., lithiumalloying or dealloying) results in cracking of the anode, a decline ofelectrochemical cyclic performance and diminished Coulombic chargecapacity (capacity fade), and limited cycle life.

It would be desirable to develop high performance negative electrodematerials comprising silicon or other negative-electrode materials thatexpand during lithium cycling for use in high power lithium ionbatteries, which overcome the current shortcomings that prevent theirwidespread commercial use, especially in vehicle applications. For longterm and effective use, anode materials containing silicon should becapable of minimal capacity fade and maximized charge capacity forlong-term use in lithium ion batteries.

SUMMARY

This section provides a general summary of the disclosure, and is not acomprehensive disclosure of its full scope or all of its features.

In certain aspects, a negative electrode material for a lithium-ionelectrochemical cell is provided. The negative electrode material maycomprise a polymeric ultrathin conformal coating formed on a surface ofa negative electroactive material. In certain aspects, the negativeelectroactive material may be selected from the group consisting of:silicon, silicon-containing alloys, tin-containing alloys, andcombinations thereof. The coating has a thickness of less than or equalto about 50 nm. The coating may be flexible and thus capable ofreversibly elongating by at least 50% from a contracted state to anexpanded state in at least one direction to minimize or preventfracturing of the negative electroactive material during lithium ioncycling.

In other aspects, the present disclosure provides a method of making anegative electrode for an electrochemical cell. The method comprisespolymerizing one or more precursors on a surface of a negativeelectroactive material. The negative electroactive material may beselected from the group consisting of: silicon, silicon-containingalloys, tin-containing alloys, and combinations thereof. Thepolymerizing forms a polymeric ultrathin conformal coating having athickness of less than or equal to about 50 nm. The coating may beflexible and capable of reversibly elongating at least 50% from acontracted state to an expanded state in at least one direction tominimize or prevent fracturing of the negative electroactive materialduring lithium ion cycling. The polymerizing occurs by a processselected from the group consisting of: layer-by-layer polymerization,anionic polymerization, cationic polymerization, and radicalpolymerization.

Further areas of applicability will become apparent from the descriptionprovided herein. The description and specific examples in this summaryare intended for purposes of illustration only and are not intended tolimit the scope of the present disclosure.

DRAWINGS

The drawings described herein are for illustrative purposes only ofselected embodiments and not all possible implementations, and are notintended to limit the scope of the present disclosure.

FIG. 1 is a schematic of an exemplary electrochemical battery cell;

FIG. 2 is a schematic showing volumetric expansion of an electroactivematerial comprising silicon during lithium ion intercalation/alloying.

FIG. 3 is a schematic showing an electrode material in anelectrochemical cell comprises an ultrathin conformal coating preparedin accordance with certain aspects of the present disclosure that iscapable of minimizing or preventing fracturing of the electrode materialduring lithium ion cycling.

FIG. 4 shows X-Ray Photon Spectroscopy (XPS) of a polymeric ultrathinconformal coating comprising silicon deposited on a copper substrate.

FIG. 5 shows infrared spectroscopy of an organic polymeric coatingcomprising a siloxane applied to a silicon surface.

FIG. 6 shows comparative electrochemical performance for a control andtwo comparative samples prepared in accordance with certain aspects ofthe present disclosure having a polymeric ultrathin conformal coating onsilicon at thicknesses of 5 nm and 10 nm.

Corresponding reference numerals indicate corresponding parts throughoutthe several views of the drawings.

DETAILED DESCRIPTION

Example embodiments are provided so that this disclosure will bethorough, and will fully convey the scope to those who are skilled inthe art. Numerous specific details are set forth such as examples ofspecific compositions, components, devices, and methods, to provide athorough understanding of embodiments of the present disclosure. It willbe apparent to those skilled in the art that specific details need notbe employed, that example embodiments may be embodied in many differentforms and that neither should be construed to limit the scope of thedisclosure. In some example embodiments, well-known processes,well-known device structures, and well-known technologies are notdescribed in detail.

The terminology used herein is for the purpose of describing particularexample embodiments only and is not intended to be limiting. As usedherein, the singular forms “a,” “an,” and “the” may be intended toinclude the plural forms as well, unless the context clearly indicatesotherwise. The terms “comprises,” “comprising,” “including,” and“having,” are inclusive and therefore specify the presence of statedfeatures, elements, compositions, steps, integers, operations, and/orcomponents, but do not preclude the presence or addition of one or moreother features, integers, steps, operations, elements, components,and/or groups thereof. Although the open-ended term “comprising,” is tobe understood as a non-restrictive term used to describe and claimvarious embodiments set forth herein, in certain aspects, the term mayalternatively be understood to instead be a more limiting andrestrictive term, such as “consisting of” or “consisting essentially of”Thus, for any given embodiment reciting compositions, materials,components, elements, features, integers, operations, and/or processsteps, the present disclosure also specifically includes embodimentsconsisting of, or consisting essentially of, such recited compositions,materials, components, elements, features, integers, operations, and/orprocess steps. In the case of “consisting of” the alternative embodimentexcludes any additional compositions, materials, components, elements,features, integers, operations, and/or process steps, while in the caseof “consisting essentially of” any additional compositions, materials,components, elements, features, integers, operations, and/or processsteps that materially affect the basic and novel characteristics areexcluded from such an embodiment, but any compositions, materials,components, elements, features, integers, operations, and/or processsteps that do not materially affect the basic and novel characteristicscan be included in the embodiment.

Any method steps, processes, and operations described herein are not tobe construed as necessarily requiring their performance in theparticular order discussed or illustrated, unless specificallyidentified as an order of performance. It is also to be understood thatadditional or alternative steps may be employed, unless otherwiseindicated.

When a component, element, or layer is referred to as being “on,”“engaged to,” “connected to,” or “coupled to” another element or layer,it may be directly on, engaged, connected or coupled to the othercomponent, element, or layer, or intervening elements or layers may bepresent. In contrast, when an element is referred to as being “directlyon,” “directly engaged to,” “directly connected to,” or “directlycoupled to” another element or layer, there may be no interveningelements or layers present. Other words used to describe therelationship between elements should be interpreted in a like fashion(e.g., “between” versus “directly between,” “adjacent” versus “directlyadjacent,” etc.). As used herein, the term “and/or” includes any and allcombinations of one or more of the associated listed items.

Although the terms first, second, third, etc. may be used herein todescribe various steps, elements, components, regions, layers and/orsections, these steps, elements, components, regions, layers and/orsections should not be limited by these terms, unless otherwiseindicated. These terms may be only used to distinguish one step,element, component, region, layer or section from another step, element,component, region, layer or section. Terms such as “first,” “second,”and other numerical terms when used herein do not imply a sequence ororder unless clearly indicated by the context. Thus, a first step,element, component, region, layer or section discussed below could betermed a second step, element, component, region, layer or sectionwithout departing from the teachings of the example embodiments.

Spatially or temporally relative terms, such as “before,” “after,”“inner,” “outer,” “beneath,” “below,” “lower,” “above,” “upper,” and thelike, may be used herein for ease of description to describe one elementor feature's relationship to another element(s) or feature(s) asillustrated in the figures. Spatially or temporally relative terms maybe intended to encompass different orientations of the device or systemin use or operation in addition to the orientation depicted in thefigures.

Throughout this disclosure, the numerical values represent approximatemeasures or limits to ranges to encompass minor deviations from thegiven values and embodiments having about the value mentioned as well asthose having exactly the value mentioned. Other than in the workingexamples provided at the end of the detailed description, all numericalvalues of parameters (e.g., of quantities or conditions) in thisspecification, including the appended claims, are to be understood asbeing modified in all instances by the term “about” whether or not“about” actually appears before the numerical value. “About” indicatesthat the stated numerical value allows some slight imprecision (withsome approach to exactness in the value; approximately or reasonablyclose to the value; nearly). If the imprecision provided by “about” isnot otherwise understood in the art with this ordinary meaning, then“about” as used herein indicates at least variations that may arise fromordinary methods of measuring and using such parameters. For example,“about” may comprise a variation of less than or equal to 5%, optionallyless than or equal to 4%, optionally less than or equal to 3%,optionally less than or equal to 2%, optionally less than or equal to1%, optionally less than or equal to 0.5%, and in certain aspects,optionally less than or equal to 0.1%.

In addition, disclosure of ranges includes disclosure of all values andfurther divided ranges within the entire range, including endpoints andsub-ranges given for the ranges.

Example embodiments will now be described more fully with reference tothe accompanying drawings.

The present technology pertains to improved electrochemical cells,including batteries, especially lithium ion batteries and lithium sulfurbatteries that may be used in vehicle applications. An exemplary andschematic illustration of a battery 20 is shown in FIG. 1. The batterymay be a lithium ion electrochemical cell or a lithium sulfurelectrochemical cell. The battery 20 includes a negative electrode 22, apositive electrode 24, and a separator 26 (e.g., a microporous polymericseparator) disposed between the two electrodes 22, 24. The separator 26comprises an electrolyte 30, which may also be present in the negativeelectrode 22 and positive electrode 24. A negative electrode currentcollector 32 may be positioned at or near the negative electrode 22 anda positive electrode current collector 34 may be positioned at or nearthe positive electrode 24. The negative electrode current collector 32and positive electrode current collector 34 respectively collect andmove free electrons to and from an external circuit 40. An interruptibleexternal circuit 40 and load 42 connects the negative electrode 22(through its current collector 32) and the positive electrode 24(through its current collector 34). Each of the negative electrode 22,the positive electrode 24, and the separator 26 may further comprise theelectrolyte 30 capable of conducting lithium ions. The separator 26operates as both an electrical insulator and a mechanical support, bybeing sandwiched between the negative electrode 22 and the positiveelectrode 24 to prevent physical contact and thus, the occurrence of ashort circuit. The separator 26, in addition to providing a physicalbarrier between the two electrodes 22, 24, can provide a minimalresistance path for internal passage of lithium ions (and relatedanions) for facilitating functioning of the battery 20.

The battery 20 can generate an electric current during discharge by wayof reversible electrochemical reactions that occur when the externalcircuit 40 is closed (to connect the negative electrode 22 and thepositive electrode 34) when the negative electrode 22 contains arelatively greater quantity of intercalated/diffused lithium. Thechemical potential difference between the positive electrode 24 and thenegative electrode 22 drives electrons produced by the oxidation ofintercalated/diffused lithium at the negative electrode 22 through theexternal circuit 40 toward the positive electrode 24. Lithium ions,which are also produced at the negative electrode, are concurrentlytransferred through the electrolyte 30 and separator 26 towards thepositive electrode 24. The electrons flow through the external circuit40 and the lithium ions migrate across the separator 26 in theelectrolyte 30 to form intercalated lithium at the positive electrode24. The electric current passing through the external circuit 18 can beharnessed and directed through the load device 42 until theintercalated/diffused lithium in the negative electrode 22 is depletedand the capacity of the battery 20 is diminished.

The battery 20 can be charged or re-powered at any time by connecting anexternal power source to the lithium ion battery 20 to reverse theelectrochemical reactions that occur during battery discharge. Theconnection of an external power source to the battery 20 compels theotherwise non-spontaneous oxidation of intercalated lithium at thepositive electrode 24 to produce electrons and lithium ions. Theelectrons, which flow back towards the negative electrode 22 through theexternal circuit 40, and the lithium ions, which are carried by theelectrolyte 30 across the separator 26 back towards the negativeelectrode 22, reunite at the negative electrode 22 and replenish it withintercalated/diffused lithium for consumption during the next batterydischarge cycle. The external power source that may be used to chargethe battery 20 may vary depending on the size, construction, andparticular end-use of the battery 20. Some notable and exemplaryexternal power sources include, but are not limited to, an AC walloutlet and a motor vehicle alternator. In many lithium ion battery andlithium sulfur battery configurations, each of the negative currentcollector 32, negative electrode 22, the separator 26, positiveelectrode 24, and positive current collector 34 are prepared asrelatively thin layers (for example, several micrometers or a millimeteror less in thickness) and assembled in layers connected in electricalparallel arrangement to provide a suitable energy package.

Furthermore, the battery 20 can include a variety of other componentsthat while not depicted here are nonetheless known to those of skill inthe art. For instance, the lithium ion battery 20 may include a casing,gaskets, terminal caps, and any other conventional components ormaterials that may be situated within the battery 20, including betweenor around the negative electrode 22, the positive electrode 24, and/orthe separator 26, by way of non-limiting example. As noted above, thesize and shape of the battery 20 may vary depending on the particularapplication for which it is designed. Battery-powered vehicles andhand-held consumer electronic devices, for example, are two exampleswhere the battery 20 would most likely be designed to different size,capacity, and power-output specifications. The battery 20 may also beconnected in series or parallel with other similar lithium ion cells orbatteries to produce a greater voltage output and power density if it isrequired by the load device 42.

Accordingly, the battery 20 can generate electric current to a loaddevice 42 that can be operatively connected to the external circuit 40.The load device 42 may be powered fully or partially by the electriccurrent passing through the external circuit 40 when the lithium ionbattery 20 is discharging. While the load device 42 may be any number ofknown electrically-powered devices, a few specific examples ofpower-consuming load devices include an electric motor for a hybridvehicle or an all-electrical vehicle, a laptop computer, a tabletcomputer, a cellular phone, and cordless power tools or appliances, byway of non-limiting example. The load device 42 may also be apower-generating apparatus that charges the battery 20 for purposes ofstoring energy.

Any appropriate electrolyte 30, whether in solid form or solution,capable of conducting lithium ions between the negative electrode 22 andthe positive electrode 24 may be used in the lithium ion battery 20. Incertain aspects, the electrolyte solution may be a non-aqueous liquidelectrolyte solution that includes a lithium salt dissolved in anorganic solvent or a mixture of organic solvents. Numerous conventionalnon-aqueous liquid electrolyte 30 solutions may be employed in thelithium ion battery 20. A non-limiting list of lithium salts that may bedissolved in an organic solvent to form the non-aqueous liquidelectrolyte solution include LiPF₆, LiClO₄, LiAlCl₄, LiI, LiBr, LiSCN,LiBF₄, LiB(C₆H₅)₄, LiAsF₆, LiCF₃SO₃, LiN(CF₃SO₂)₂, and combinationsthereof. These and other similar lithium salts may be dissolved in avariety of organic solvents, including but not limited to various alkylcarbonates, such as cyclic carbonates (ethylene carbonate (EC),propylene carbonate (PC), butylene carbonate(BC)), acyclic carbonates(dimethyl carbonate (DMC), diethyl carbonate (DEC), ethylmethylcarbonate(EMC)), aliphatic carboxylic esters (methyl formate, methyl acetate,methyl propionate), γ-lactones (γ-butyrolactone, γ-valerolactone), chainstructure ethers (1,2-dimethoxyethane, 1-2-diethoxyethane,ethoxymethoxyethane), cyclic ethers (tetrahydrofuran,2-methyltetrahydrofuran), and mixtures thereof.

The separator 26 may comprise, in one embodiment, a microporouspolymeric separator comprising a polyolefin. The polyolefin may be ahomopolymer (derived from a single monomer constituent) or aheteropolymer (derived from more than one monomer constituent), whichmay be either linear or branched. If a heteropolymer is derived from twomonomer constituents, the polyolefin may assume any copolymer chainarrangement, including those of a block copolymer or a random copolymer.Similarly, if the polyolefin is a heteropolymer derived from more thantwo monomer constituents, it may likewise be a block copolymer or arandom copolymer. In certain aspects, the polyolefin may be polyethylene(PE), polypropylene (PP), or a blend of PE and PP.

When the separator 26 is a microporous polymeric separator, it may be asingle layer or a multi-layer laminate, which may be fabricated fromeither a dry or wet process. For example, in one embodiment, a singlelayer of the polyolefin may form the entire microporous polymerseparator 26. In other aspects, the separator 26 may be a fibrousmembrane having an abundance of pores extending between the opposingsurfaces and may have a thickness of less than a millimeter, forexample. As another example, however, multiple discrete layers ofsimilar or dissimilar polyolefins may be assembled to form themicroporous polymer separator 26. The microporous polymer separator 26may also comprise other polymers in addition to the polyolefin such as,but not limited to, polyethylene terephthalate (PET), polyvinylidenefluoride (PVDF), cellulose, and/or a polyamide. The polyolefin layer,and any other optional polymer layers, may further be included in themicroporous polymer separator 26 as a fibrous layer to help provide themicroporous polymer separator 26 with appropriate structural andporosity characteristics. Various conventionally available polymers andcommercial products for forming the separator 26 are contemplated, aswell as the many manufacturing methods that may be employed to producesuch a microporous polymer separator 26.

In a lithium ion battery, the positive electrode 24 may be formed from alithium-based active material that can sufficiently undergo lithiumintercalation and deintercalation while functioning as the positiveterminal of the lithium ion battery 20. The positive electrode 24 mayinclude a polymeric binder material to structurally fortify thelithium-based active material. One exemplary common class of knownmaterials that can be used to form the positive electrode 24 is layeredlithium transitional metal oxides. For example, in certain embodiments,the positive electrode 24 may comprise at least one spinel comprising atransition metal like lithium manganese oxide (Li_((1+x))Mn_((2−x))O₄),where 0≤x≤1, where x is typically less than 0.15, including LiMn₂O₄,lithium manganese nickel oxide (LiMn_((2−x))Ni_(x)O₄), where 0≤x≤1(e.g., LiMn_(1.5)Ni_(0.5)O₄), lithium cobalt oxide (LiCoO₂), lithiummanganese oxide (LiMn₂O₄), lithium nickel oxide (LiNiO₂), a lithiumnickel manganese cobalt oxide (Li(Ni_(x)Mn_(y)Co_(z))O₂), where 0≤x≤1,0≤y≤1, 0≤z≤1, and x+y+z=1, including LiMn_(0.33)Ni_(0.33)Co_(0.33)O₂, alithium nickel cobalt metal oxide (LiNi_((1−x−y))Co_(x)M_(y)O₂), where0<x<1, y<1, and M may be Al, Mn, or the like, other knownlithium-transition metal oxides or mixed oxides lithium iron phosphates,or a lithium iron polyanion oxide such as lithium iron phosphate(LiFePO₄) or lithium iron fluorophosphate (Li₂FePO₄F). Such activematerials may be intermingled with at least one polymeric binder, forexample, by slurry casting active materials with such binders, likepolyvinylidene fluoride (PVDF), ethylene propylene diene monomer (EPDM)rubber, or carboxymethoxyl cellulose (CMC). The positive currentcollector 34 may be formed from aluminum or any other appropriateelectrically conductive material known to those of skill in the art.

In a lithium sulfur battery, the positive electrode includessulfur-based compounds for a positive active material. A sulfur-basedcompound may be selected from at least one of: elemental sulfur,Li₂S_(n) (wherein n greater than or equal to 1), Li₂S_(n) (wherein ngreater than or equal to 1) dissolved in a catholyte, an organosulfurcompound, and a carbon-sulfur polymer ((C₂S_(x))_(n): wherein x=2.5, andn is 2 or greater). The positive electrode may also include electricallyconductive materials that facilitate the movement of the electronswithin the positive electrode. For example, electrically conductivematerials may include graphite, carbon-based materials, or a conductivepolymer. Carbon-based materials may include by way of non-limitingexample Ketchen black, Denka black, acetylene black, carbon, black, andthe like. Examples of a conductive polymer include polyaniline,polythiophene, polyacetylene, polypyrrole, and the like. The conductivematerial may be used alone or as a mixture of two or more materials. Thepositive electrode may also include a polymeric binder as describedabove.

In certain aspects, the present disclosure provides improved negativeelectrodes (e.g., anode). The electrochemically active negativeelectrode material may be selected from the group consisting of:silicon, silicon-containing alloys, tin-containing alloys, andcombinations thereof. By way of example, particles comprising siliconmay include silicon, or silicon containing binary and ternary alloysand/or tin-containing alloys, such as Si—Sn, SiSnFe, SiSnAl, SiFeCo,SnO₂, and the like. Such negative electrode materials suffer fromsignificant volumetric expansion during lithium cycling (e.g., capableof accepting the insertion of lithium ions during charging of theelectrochemical cell “intercalation” and releasing lithium ions duringdischarging of the electrochemical cell “deintercalation” or lithiumalloying/dealloying).

For example, as shown in FIG. 2, a particle 100 comprising asilicon-containing material undergoes a significant volume expansionduring lithium ion intercalation or lithium alloying. In an initialstate 110 prior to lithium ion insertion or reaction, the particle 100is in a first contracted state. After lithium ioninsertion/intercalation or alloying, the particle 100 is in a secondexpanded state 120. For example, where the particle is a siliconparticle (Si) in the first contracted state 110, after lithium ioninsertion it forms Li_(4.4)Si (corresponding to the second expandedstate 120). The volume of a silicon particle 100 after lithium insertionin the second expanded state 120 may be up to four (4) times (400%)larger than the volume of silicon particle 100 in the first contractedstate 110. As will be appreciated, the first contracted state 110 maycorrespond to the volume of the particle 100 before lithium insertion orafter lithium extraction. In a conventional system like that shown inFIG. 2, the extent of volumetric expansion that occurs can cause theparticle 100 to transition into a third state 130 where the particle 100mechanically degrades and breaks into a plurality of smaller fragmentsor pieces 132. When the particle 100 breaks into smaller pieces 132 inthe third state 130, these fragments or smaller pieces 132 can no longermaintain performance of the electrochemical cell. Thus, it is desirableto avoid the fragmentation and breakage associated with the third state130.

In accordance with various aspects of the present teachings, anelectrode material in an electrochemical cell comprises an ultrathinconformal coating that is capable of minimizing or preventing fracturingof the negative electrode material during lithium ion cycling. Forexample, as shown in FIG. 3, an electrode material particle 140 has anultrathin polymeric flexible conformal coating 142 disposed thereon. Thecoating is polymeric, thus comprising at least one polymer or oligomerincluding a siloxane unit (e.g., —SiO—) and/or an organic unit (e.g.,—CH_(n)—). In certain variations, the polymer comprises silicon, forexample, a siloxane unit. It should be noted that the features in FIG. 3are not necessarily shown to scale, but rather are merely provided forpurposes of illustration.

The ultrathin conformal coating is applied to exposed regions of asurface of the electrode material, meaning that it is thin butextensively covers the exposed regions of the surface of the material.In certain variations, the polymeric ultrathin conformal coating isdisposed on greater than or equal to about 50% of the exposed surfacearea of the negative electrode material, optionally on greater than orequal to about 75% of the exposed surface area, optionally on greaterthan or equal to about 90% of the exposed surface area, optionally ongreater than or equal to about 95% of the exposed surface area,optionally on greater than or equal to about 97% of the exposed surfacearea, optionally on greater than or equal to about 98% of the exposedsurface area, optionally on greater than or equal to about 99% of theexposed surface area, optionally on greater than or equal to about 99.5%of the exposed surface area, and in certain aspects, 100% of the exposedsurface area of the negative electrode material of the negativeelectrode material is coated with the polymeric ultrathin conformalcoating.

In certain preferred aspects, a surface of a negative electrode materialcomprising silicon and/or tin has an ultrathin conformal surface coatingthat is flexible and minimizes or prevents fracturing of the negativeelectrode material during lithium ion cycling in the electrochemicalcell. If minor degradation of the active electrode material occurs, theflexible polymer coating can assist in maintaining the structuralintegrity of the electrode. In certain variations, an average thicknessof the surface coating on the negative electrode material is ultrathinand thus has an average thickness of less than or equal to about 50 nm,optionally less than or equal to about 35 nm, optionally less than orequal to about 30 nm, optionally less than or equal to about 25 nm,optionally less than or equal to about 20 nm, optionally less than orequal to about 15 nm, optionally less than or equal to about 10 nm,optionally less than or equal to about 9 nm, optionally less than orequal to about 8 nm, optionally less than or equal to about 7 nm, andoptionally less than or equal to about 6 nm. In certain variations, anultrathin coating is greater than or equal to about 5 nm to less than orequal to about 50 nm.

In certain variations, a thickness of the ultrathin conformal surfacecoating only deviates across the surface of the electroactive material amaximum amount of less than or equal to about 100% (a difference inthickness from the thinnest portion of the coating to the thickestportion of the coating is ≤100%). In this manner, the thickness of thecoating is relatively uniform and maintains coverage over the surface ofthe electrode material in the expanded state, as well as in thecontracted state. The ultrathin conformal surface coating providessufficient coverage of the exposed surface regions to maintain and keepthe negative electrode material that undergoes high volumetric expansionintact without fracturing and diminishing performance in theelectrochemical cell, while maintaining lithium ion diffusion levels andminimizing electrical impedance at the electroactive material surface toincrease electrode integrity.

In certain aspects, the polymeric ultrathin conformal coating isflexible and thus capable of reversibly elongating by at least 50% froma contracted state to an expanded state in at least one direction tominimize or prevent fracturing of the negative electrode material orholding the fractured electrode particles together to maintain bothionic and electrical conductivity during lithium ion cycling. In certainvariations, a modulus of elasticity of the polymeric ultrathin conformalcoating may be less than or equal to about 2 GPa when the coating issaturated with liquid electrolyte, and in certain preferred variations,less than or equal to about 1 GPa. By reversibly elongating in at leastone direction, it is meant that the polymeric conformal coating canexpand and contract in at least one direction from an initial point(e.g., initial length L_(i)) to an expanded point (e.g., expanded lengthL_(e)) and return to or at least near to the initial point withoutmechanical fracture or failure. Thus, an elongation of at least 50%means that L_(e)−L_(i)/L_(i)≥50%, so that in an example where an initialaverage thickness of the ultrathin conformal coating corresponds to anLi of 5 nm, 50% elongation would amount to an expanded length L_(e) ofabout 7.5 nm. In this manner, the flexible polymeric ultrathin conformalcoating provides the ability to expand and contract with the electrodeactive material during lithium cycling. Depending on the electroactivematerial used, the ultrathin conformal coating may be capable ofreversibly elongating by at least 75% from a contracted state to anexpanded state in at least one direction, optionally by at least 100%from a contracted state to an expanded state in at least one direction,optionally by at least 125% from a contracted state to an expanded statein at least one direction, optionally by at least 150%, optionally by atleast 175%, and in certain variations up to or exceeding 200% elongationfrom a contracted state to an expanded state in at least one directionto minimize or prevent fracturing of the negative electrode materialduring lithium ion cycling. The ultrathin conformal coating polymericdesirably has a lithium ion conductivity or diffusion rate that isgreater than that of the electrode material, for example, greater than10⁻¹² to 10⁻¹⁴ cm²/s.

In certain variations, the average particle diameter of the negativeelectrode active material may be greater than or equal to about 5nanometers to less than or equal to about 200 nanometers. As notedabove, the present technology is particularly suitable for use withnegative electroactive materials for the negative electrode 22 that areselected from the group consisting of: silicon, silicon-containingalloys, tin-containing alloys, and combinations thereof. Materials thatcan be used to form the negative electrode 22 include, for example,lithium-silicon and silicon containing binary and ternary alloys and/ortin-containing alloys, such as Si—Sn, SiSnFe, SiSnAl, SiFeCo, SnO₂, andthe like. Negative electrodes may comprise greater than or equal toabout 50% to less than or equal to about 90% of an electroactivematerial (e.g., silicon-containing or tin-containing particles),optionally greater than or equal to about 5% to less than or equal toabout 30% of an electrically conductive material, and a balance binder.Suitable electrically conductive materials may be selected from graphiteparticles, carbon black, powdered nickel, metal particles, conductivepolymers, and combinations thereof. Useful binders may comprise apolymeric material and extractable plasticizer suitable for forming abound porous composite, such as halogenated hydrocarbon polymers (suchas poly(vinylidene chloride) and poly((dichloro-1,4-phenylene)ethylene),fluorinated urethanes, fluorinated epoxides, fluorinated acrylics,copolymers of halogenated hydrocarbon polymers, epoxides, ethylenepropylene diamine termonomer (EPDM), ethylene propylene diaminetermonomer (EPDM), polyvinylidene difluoride (PVDF), hexafluoropropylene(HFP), ethylene acrylic acid copolymer (EAA), ethylene vinyl acetatecopolymer (EVA), EAA/EVA copolymers, PVDF/HFP copolymers, CMC (carboxylmethyl cellulose) and mixtures thereof. The negative electrode currentcollector 32 may be formed from copper or any other appropriateelectrically conductive material known to those of skill in the art.

An electrode may be made by mixing the electrode active material, suchas silicon-containing particles having a polymeric ultrathin conformalcoating, into a slurry with a polymeric binder compound, a non-aqueoussolvent, optionally a plasticizer, and optionally if necessary,electrically conductive particles. The slurry can be mixed or agitated,and then thinly applied to a substrate via a doctor blade. The substratecan be a removable substrate or alternatively a functional substrate,such as a current collector (such as a metallic grid or mesh layer)attached to one side of the electrode film. In one variation, heat orradiation can be applied to evaporate the solvent from the electrodefilm, leaving a solid residue. The electrode film may be furtherconsolidated, where heat and pressure are applied to the film to sinterand calendar it. In other variations, the film may be air-dried atmoderate temperature to form self-supporting films. If the substrate isremovable, then it is removed from the electrode film that is thenfurther laminated to a current collector. With either type of substrateit may be necessary to extract or remove the remaining plasticizer priorto incorporation into the battery cell.

In certain preferred variations, pre-fabricated electrodes formed ofsilicon-containing particles via the active material slurry castingdescribed above can be directly coated via a coating formation process,such as in atomic layer deposition (ALD), or physical vapor deposition,or chemical vapor infiltration. Thus, one or more exposed regions of thepre-fabricated negative electrodes comprising the electroactive materialparticles can be coated on the surfaces of negative electrode materialswhen incorporated into the electrochemical cell. In other variations, aplurality of particles comprising an electroactive material can becoated with a polymeric ultrathin conformal coating. Then, the coatedparticles can be used in the active material slurry to form the negativeelectrode, as described above.

A battery may thus be assembled in a laminated cell structure,comprising an anode layer, a cathode layer, and electrolyte/separatorbetween the anode and cathode layers. The anode and cathode layers eachcomprise a current collector. A negative anode current collector may bea copper collector foil, which may be in the form of an open mesh gridor a thin film. The current collector can be connected to an externalcurrent collector tab.

For example, in certain variations, an electrode membrane, such as ananode membrane, comprises the electrode active material (e.g., silicon)dispersed in a polymeric binder matrix over a current collector. Theseparator can then be positioned over the negative electrode element,which is covered with a positive electrode membrane comprising acomposition of a finely divided lithium insertion compound in apolymeric binder matrix. A positive current collector, such as aluminumcollector foil or grid completes the assembly. Tabs of the currentcollector elements form respective terminals for the battery. Aprotective bagging material covers the cell and prevents infiltration ofair and moisture. Into this bag, an electrolyte is injected into theseparator (and may also be imbibed into the positive and/or negativeelectrodes) suitable for lithium ion transport. In certain aspects, thelaminated battery is further hermetically sealed prior to use.

Thus, in certain variations, the present disclosure provides anelectroactive material, which may be used in an electrochemical cell,such as a lithium-ion battery. A negative electrode material maycomprise silicon, silicon alloys, tin, and their alloys, for example. Incertain variations, the negative electrode material comprises silicon.The electrode material has a polymeric ultrathin conformal surfacecoating formed thereon, which may have a thickness of less than or equalto about 50 nm and is capable of reversibly elongating by at least 50%from a contracted state to an expanded state in at least one directionto minimize or prevent fracturing of the negative electrode materialduring lithium ion cycling within the electrochemical cell. In certainvariations, the electroactive material comprising silicon, siliconalloys, tin, and their alloys is contained in a pre-fabricated electrodelayer and the polymeric ultrathin conformal coating is applied to atleast one surface of the pre-fabricated electrode layer. In othervariations, the polymeric ultrathin conformal coating is applied to aplurality of particles comprising silicon, silicon alloys, tin, andtheir alloys, which can then subsequently be incorporated into theelectrode. In certain preferred aspects, the polymeric coating comprisessilicon, for example, a siloxane or siloxane copolymer. In certainaspects, the polymeric ultrathin conformal coating is ultrathin andformed in an atomic layer deposition process.

In other aspects, the present disclosure provides a method of making anegative electrode for an electrochemical cell that includes apolymerizing process, where one or more precursors are reacted on asurface of a negative electrode material selected from the groupconsisting of: silicon, silicon-containing alloys, tin-containingalloys, and combinations thereof. The precursor may be an initiator or amonomer in certain variations. The polymerizing forms a polymericultrathin conformal coating as described above. The polymerizing mayoccur by a process selected from the group consisting of: layer-by-layerpolymerization, which may be conducted as vapor reactants via atomiclayer deposition, anionic polymerization, cationic polymerization, andradical polymerization. The polymerizing may be conducted in a processselected from the group consisting of: atomic layer deposition (ALD),physical vapor deposition (PVD), chemical vapor deposition (CVD),molecular layer deposition (MLD), layer by layer deposition (LBL),chemical vapor infiltration, and wet chemistry.

In one variation, the polymerizing process comprises a layer-by-layerpolymerization. In certain aspects, the layer-by-layer process may occurin an atomic layer deposition (ALD) reactor, where a first gaseousprecursor (e.g., an alkyl lithium like lithium tert-butoxide-LiO^(t)Bu)and a second gaseous precursor (e.g., a linear or cyclic siloxane) aresequentially introduced to the reactor. The linear or cyclic siloxanesmay include linear siloxane polymers [—SiRR′O—] (with various alkyl andaryl R and R′ side groups), silsesquioxanes polymers, silalkylenepolymers [—Si(CH₃)₂(CH₂)_(m)—], and any copolymers of the above. In oneexample, the second gaseous precursor may be a cyclic methyl siloxane.Trimethylaluminum (TMA) may also be used as a precursor. With alkyllithium as an initiator, the cyclic siloxane or linear siloxanes can bepolymerized into the polymer coating in situ on the particles or anyother substrates for a variety of applications.

In certain variations, a suitable gaseous polymerization/depositionprocess for layer-by-layer polymerization includes atomic layerdeposition (ALD), where first the first gaseous precursor is applied tothe surface of the negative electrode material. In any of the methodsdescribed herein, the negative electrode material desirably has at least1% of the exposed surface area with active hydrogen or hydroxyl groups.This amount of active groups on the surface helps to ensure surfacecoverage levels with the polymeric coating discussed previously above,for example, greater than 90% of the exposed surface area being coveredby the polymeric coating. If necessary, the surface of the electrodeactive material can be activated prior to polymerization by conventionalmethods known in the art, for example, by plasma treatment, oxidation,or other chemical treatment. Thus, in this polymerization process, thepolymeric ultrathin conformal surface coating is built up layer-by-layerso that the first gaseous precursor is initially reacted with the activegroups on the surface of the negative electrode material.

In one exemplary process, the deposition temperature for the substratemay be about 80° C. The heating temperature for precursorstrimethylaluminum (TMA) and cyclic methyl siloxane may also be around80° C., and the heating temperature for precursor lithium tert-butoxideis around 160° C. A flow rate of the carry gas (Ar) is around 20 SCCM.For each precursor, the initial purge time is around 0.015 seconds, theexposure time is approximately 20 seconds, and the purge time isapproximately 20 seconds. All the precursors are alternatively input thedeposition chamber; each precursor goes through purge-expose-pump, whichleads to one cycle. In one cycle, a thickness of the polymer coating isaround 0.15 nm. The coating thickness is controlled by the number ofcycles used, where thicker coatings may be formed by increasing thenumber of cycles conducted. The polymeric ultrathin conformal coatingthus formed comprises a siloxane polymer.

In other variations, the polymerizing process comprises a radicalpolymerization process. The precursors may include an initiator and amonomer. While the precursors can be in either gas/vapor or liquidstates, in most cases, the precursors are in a vapor or gas statebecause of the temperatures to which they are heated and that the carrygas (e.g., Ar) brings them into the reactor. In certain variations, theinitiator is selected from the group consisting of: azoisobutylnitrile,dicumyl peroxide, persulfate, and combinations thereof. The monomer maycomprise an acrylate monomer or a methacrylate monomer. In certainvariations, the monomer may be4-Methacryloyloxy-2,2,6,6-tetramethylpiperidine-1-oxy (TEMPOmethacrylate, which forms a semiconducting polymer). Such a radicalpolymerization process is conducted in an oxygen-free and water-freeenvironment. For example, the radical polymerization process may beconducted in an inert gas environment (e.g., nitrogen, argon). Theinitiator, monomer, and the active particles are blended together andreacted at suitable temperatures to achieve the coating layer on theparticle surface. Thus, in certain variations, the polymeric ultrathinconformal coating formed comprises a semi-conductive methacrylatepolymer.

In yet other variations, the polymerizing process comprises anionicpolymerization. The precursors may include an initiator and a monomer.While the precursors can be in either gas/vapor or liquid states, inmost cases, the precursors are in a vapor or gas state because of thetemperatures to which they are heated and that the carry gas (e.g., Ar)brings them into the reactor. In certain variations, the initiator isselected from the group consisting of: Grignard reagents, metalalkoxides, amides, cyanides, and combinations thereof. Suitable examplesof such initiators may include sec-Butyl lithium, diphenyl methyl Na,and NaNH₂. The monomer may be selected from the group consisting of:vinyl pyridine, cyclic siloxane, cyanoacrylate, propylene oxide, vinylsilane, and combinations thereof. Suitable examples of such monomers mayinclude vinyl pyridine, cyclic siloxane with various alkyl and arylgroups, such as methyl, ethyl, phenyl, and the like. Such an anionicpolymerization process may be conducted in an oxygen-free and water-freeenvironment. For example, the anionic polymerization process may beconducted in an inert gas environment (e.g., nitrogen, argon). Thus, incertain variations, the polymeric ultrathin conformal coating formedcomprises a polymer selected from the group consisting of: vinylpyridine, cyclic dimethyl siloxane, and combinations thereof.

In yet further variations, the polymerizing process may comprisecationic polymerization. The precursors may include an initiator and amonomer. While the precursors can be in either gas/vapor or liquidstates, in most cases, the precursors are in a vapor or gas statebecause of the temperatures to which they are heated and that the carrygas (e.g., Ar) brings them into the reactor. In certain variations, theinitiator is a protonic acid. Suitable examples of such an initiator mayinclude phosphoric, sulfuric, fluoro-, and triflic(trifluoromethanesulfonic) acids. Other initiators may be Lewis acids,such as SnCl₄, AlCl₃, BF₃, and TiCl₄. The monomer may be selected fromthe group consisting of: lactones, lactams, and combinations thereof.Suitable examples of such monomers may include oxirane, oxazoline, andtetrahydrofuran. Such a cationic polymerization process may be conductedin an oxygen-free and water-free environment. For example, the radicalpolymerization process may be conducted in an inert gas environment(e.g., nitrogen, argon). Thus, in certain variations, the polymericultrathin conformal coating formed comprises a polymer such aspolycaprolactam (or nylon) or polyethylene oxide.

Example 1

Samples are prepared for purposes of comparison. Sample A is prepared inaccordance with certain aspects of the present teachings and includes asilicon anode material having a linear and cyclic siloxane coatingdeposited on the silicon particles by ALD. For Sample A, the siliconelectrode material is coated with linear and cyclic siloxane applied viaan atomic layer deposition aqueous process. The precursors include acyclic methyl siloxane, lithium tert-butoxide, and trimethylaluminum(TMA). The deposition temperature for the substrate may be about 80° C.The heating temperature for precursors trimethylaluminum (TMA) andcyclic methyl siloxane may also be around 80° C., and the heatingtemperature for precursor lithium tert-butoxide is around 160° C. A flowrate of the carry gas (Ar) is around 20 SCCM. For each precursor, theinitial purge time is around 0.015 seconds, the exposure time isapproximately 20 seconds, and the purge time is approximately 20seconds. All the precursors are alternatively input the depositionchamber, each precursor goes through purge-expose-pump, which leads toone cycle. A typical reaction for forming the coating is:

${{\frac{n}{4}\left\lbrack {\left( {CH}_{3} \right){SiO}} \right\rbrack}_{n}\overset{{LiO}^{t}{{Bu}{(g)}}}{\longrightarrow}\;{n\left\lbrack {\left( {CH}_{3} \right)_{2}{SiO}} \right\rbrack}_{4}}.$A siloxane layer having a thickness of about 0.15 nm is deposited ineach cycle on electrode surfaces (half inch in diameter). The totalthickness of the polymeric surface coating formed is 5 nm after 33cycles.

Structural characterization of the polymeric siloxane coatings as formedare shown in FIGS. 4 and 5. XPS results in FIG. 4 show the Si-containingpolymeric coating has been deposited on a copper substrate. X-axis (150)is binding energy (eV) while Y-axis (152) is c/s. The typical Si signal(a small peak around 103 ev) has been detected on Cu. FIG. 5 shows asiloxane coating containing Si—O and C—H bonds has been deposited on asilicon surface of the active material. X-axis (160) is wavenumber(cm⁻¹) while Y-axis (162) is absorption.

Example 2

Si thin-film electrodes (˜100 nm) are prepared by RF magnetronsputtering on copper current collectors, and tested in coin cells forelectrochemical characterization. Polymer coatings were prepared by ALDprocess described above in Example 1. A Control is a bare silicon (Si)anode material (incorporated into a negative electrode). Sample A is asilicon material having a polymeric ultrathin conformal coatingdeposited thereon via ALD (like the process described in Example 1) at athickness of 5 nm. Sample B is a silicon material having a polymericultrathin conformal coating deposited thereon via ALD (like the processdescribed in Example 1) at a thickness of 10 nm.

Battery half cells with silicon (either Control or Samples A-B) as theworking electrodes and Li foil as counter electrode are used with anelectrolyte comprising 1M LiPF₆ in 50% EC and 50% DEC and a separator.The Si electrodes (or polymer-coated Si electrodes) are used as workingelectrodes, and pure lithium metal foil as counter and referenceelectrodes in CR2032 coin cells. A separator (CELGARD™, USA) is placedbetween working electrode and lithium foil, and 1M LiPF₆ in ethylenecarbonate and dimethyl carbonate (EC:DMC 1:1 volume ratio, BASF) isemployed for the electrolyte. An uncoated portion of the electrode isconnected to an external tab. The electrolyte and separator are disposedbetween the surfaces of respective positive and negative electrodes toform a full-cell battery. The Arbin battery test system (BT-2000) isused to cycle the coin cells, using the constant-current method (with arate of C/3) and a voltage window between 0.05 V to 1.5 V. The EIS studyis conducted in two-electrode coin cells at the assigned voltage. Thecoin cells are rested for 24 hours until they are stabilized.

Electrochemical measurements are performed with the constant currentdensity of 10 mA/g⁻¹ (about C/10) based on the mass of the positiveelectrode in the working voltage window of 3 V to about 4.8 V for fullcells. A cycle test of the battery is performed. Charge discharge cyclesare repeated 20 times at ambient conditions.

The charging and discharging profiles of the electrochemical performanceof the Control and Samples A-B are shown in FIG. 6. In FIG. 6, a leftγ-axis shows capacity retention (300) which is in normalizes capacitystarting with 1 unit, a right γ-axis shows cycle efficiency % (310),while cycle number is shown on the x-axis (320). A charge rate of C/10is used and up to 20 cycles are tested. Charge capacity and dischargecapacity are shown as solid data points (Control=322, Sample A=324,Sample B=326) while Coulombic efficiency (CE) are shown as open datapoints (Control=332, Sample A=334, Sample B=336).

Different coatings (e.g., Samples A and B) show different functionality.The polymeric coatings prepared in accordance with certain aspects ofthe present disclosure show improved cycle performance as well ascoulombic efficiency. The coating thickness has an impact on the cellperformance. Thus, the ideal thickness is believed to depend on factorsincluding: the anode chemistry, particle size and coating chemistry. Thepolymeric ultrathin conformal coating improves the cycle efficiency andcapacity retention. Thus, the polymeric coatings provide improvedcycling stability of silicon anodes. It is believed that the conformalpolymeric ultrathin conformal coating provides additional mechanicalstability to the underlying electrode material to stabilize the negativeelectrode material during expansion and contraction.

In certain variations, a lithium ion battery incorporating an inventiveelectroactive material having a polymeric ultrathin conformal surfacecoating system for minimizing or preventing fracturing of the negativeelectrode material during lithium ion cycling can maintain chargecapacity within 80% of an initial charge capacity for greater than orequal to about 500 hours of battery operation, optionally greater thanor equal to about 1,000 hours of battery operation, optionally greaterthan or equal to about 1,500 hours of battery operation, and in certainaspects, greater than or equal to about 2,000 hours or longer of batteryoperation (active cycling).

In certain variations, the lithium ion battery incorporating aninventive electroactive material having a polymeric ultrathin conformalsurface coating system for minimizing or preventing fracturing of thenegative electrode material during lithium ion cycling is capable ofmaintaining charge capacity within 80% of an initial charge capacity forat least 1,000 deep discharge cycles, optionally greater than or equalto about 2,000 deep discharge cycles, optionally greater than or equalto about 3,000 deep discharge cycles, optionally greater than or equalto about 4,000 deep discharge cycles, and in certain variations,optionally greater than or equal to about 5,000 deep discharge cycles.

The foregoing description of the embodiments has been provided forpurposes of illustration and description. It is not intended to beexhaustive or to limit the disclosure. Individual elements or featuresof a particular embodiment are generally not limited to that particularembodiment, but, where applicable, are interchangeable and can be usedin a selected embodiment, even if not specifically shown or described.The same may also be varied in many ways. Such variations are not to beregarded as a departure from the disclosure, and all such modificationsare intended to be included within the scope of the disclosure.

What is claimed is:
 1. A negative electrode material for a lithium-ionelectrochemical cell comprising: a flexible polymeric ultrathinconformal coating formed on a surface of a negative electroactivematerial, wherein the flexible polymeric ultrathin conformal coatingcomprises one or more materials selected from silicon, siloxane,polycaprolactam, polyethylene oxide, and TEMPO methacrylate and theflexible polymeric ultrathin conformal coating has a thickness of lessthan or equal to about 50 nm and is capable of reversibly elongating byat least 50% from a contracted state to an expanded state in at leastone direction to minimize or prevent fracturing of the negativeelectroactive material during lithium ion cycling.
 2. The electrodematerial of claim 1, wherein the flexible polymeric ultrathin conformalcoating is disposed on greater than or equal to about 50% of exposedsurface area of the negative electrode material.
 3. The electrodematerial of claim 1, wherein the flexible polymeric ultrathin conformalcoating is disposed on greater than or equal to about 99% of exposedsurface area of the negative electrode material.
 4. The electrodematerial of claim 1, wherein the thickness is greater than or equal toabout 5 nm to less than or equal to about 50 nm.
 5. The electrodematerial of claim 1, wherein the flexible polymeric ultrathin conformalcoating comprises silicon.
 6. The electrode material of claim 1, whereinthe flexible polymeric ultrathin conformal coating comprises siloxane.7. The electrode material of claim 1, wherein the flexible polymericultrathin conformal coating comprises a polycaprolactam or apolyethylene oxide.
 8. The electrode material of claim 1, wherein theflexible polymeric ultrathin conformal coating comprises a TEMPOmethacrylate.
 9. The electrode material of claim 1, wherein the negativeelectroactive material is in the form of a plurality of particles andthe flexible polymeric ultrathin conformal coating is applied to eachrespective particle in the plurality of particles.
 10. A lithium-ionelectrochemical cell comprising: a negative electrode comprising anegative electroactive material having a flexible polymeric ultrathinconformal coating formed on a surface of the negative electroactivematerial, wherein the coating has a thickness of less than or equal toabout 50 nm and is capable of reversibly elongating by at least 50% froma contracted state to an expanded state in at least one direction tominimize or prevent fracturing of the negative electrode during lithiumion cycling; a positive electrode comprising a positive electroactivematerial comprising lithium; a separator; and an electrolyte, whereinthe flexible polymeric ultrathin coating minimizes or preventsfracturing of the negative electrode material during lithium ion cyclingto substantially maintain charge capacity of the lithium-ionelectrochemical cell for greater than or equal to about 500 hours ofoperation.
 11. The electrode material of claim 10, wherein the flexiblepolymeric ultrathin conformal coating has a modulus of elasticity ofless than or equal to about 2 GPa when saturated with the electrolyte.12. The lithium-ion electrochemical cell of claim 10, wherein theflexible polymeric ultrathin conformal coating is disposed on greaterthan or equal to about 50% of exposed surface area of the negativeelectrode material.
 13. A method of making a negative electrode for anelectrochemical cell, the method comprising: polymerizing one or moreprecursors on a surface of a negative electroactive material to form aflexible polymeric ultrathin conformal coating having a thickness ofless than or equal to about 50 nm that is capable of reversiblyelongating at least 50% from a contracted state to an expanded state inat least one direction to minimize or prevent fracturing of the negativeelectroactive material during lithium ion cycling, wherein the flexiblepolymeric ultrathin conformal coating comprises one or more materialsselected from silicon, siloxane, polycaprolactam, polyethylene oxide,and TEMPO methacrylate, and the polymerizing occurs by a processselected from the group consisting of: layer-by-layer polymerization,anionic polymerization, cationic polymerization, and radicalpolymerization.
 14. The method of claim 13, wherein the one or moreprecursors are in a gas phase during the polymerizing.
 15. The method ofclaim 13, wherein the polymerizing comprises layer-by-layer atomic layerdeposition and the one or more precursors further comprises a firstgaseous precursor of lithium tert-butoxide, a second gaseous precursorof a cyclic siloxane, and a third gaseous precursor oftrimethylaluminum.
 16. The method of claim 13, wherein the polymerizingcomprises anionic polymerization and the one or more precursors furthercomprises an initiator and a monomer, wherein the initiator is selectedfrom the group consisting of: Grignard reagents, metal alkoxides,amides, cyanides, and combinations thereof and the monomer is selectedfrom the group consisting of: cyclic siloxane, vinyl silane, andcombinations thereof.
 17. The method of claim 13, wherein thepolymerizing comprises cationic polymerization and the one or moreprecursors further comprises an initiator and a monomer, wherein theinitiator comprises a protonic acid and the monomer is selected from thegroup consisting of: lactones, lactams, and combinations thereof. 18.The method of claim 13, wherein the polymerizing comprises radicalpolymerization and the one or more precursors further comprises aninitiator and a monomer, wherein the initiator is selected from thegroup consisting of: azoisobutylnitrile, dicumyl peroxide, persulfate,and combinations thereof and the monomer comprises4-Methacryloyloxy-2,2,6,6-tetramethylpiperidine-1-oxy.
 19. The method ofclaim 13, wherein the polymerizing occurs in a process selected from thegroup consisting of: atomic layer deposition (ALD), physical vapordeposition (PVD), chemical vapor deposition (CVD), molecular layerdeposition (MLD), layer by layer deposition (LBL), chemical vaporinfiltration, and wet chemistry.
 20. The method of claim 13, wherein thepolymerizing occurs in an atomic layer deposition (ALD) process.